The Ljungström Air Preheater 1920
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Use Feedwater Economizers for Waste Heat Recovery, Energy Tips
ADVANCED MANUFACTURING PROGRAM Energy Tips: STEAM Steam Tip Sheet #3 Use Feedwater Economizers for Waste Heat Recovery Suggested Actions ■■ Determine the stack temperature A feedwater economizer reduces steam boiler fuel requirements by transferring after the boiler has been tuned heat from the flue gas to incoming feedwater. Boiler flue gases are often to manufacturer’s specifications. rejected to the stack at temperatures more than 100°F to 150°F higher than The boiler should be operating the temperature of the generated steam. Generally, boiler efficiency can at close-to-optimum excess be increased by 1% for every 40°F reduction in flue gas temperature. By air levels with all heat transfer recovering waste heat, an economizer can often reduce fuel requirements by 5% surfaces clean. to 10% and pay for itself in less than 2 years. The table provides examples of ■■ Determine the minimum the potential for heat recovery. temperature to which stack gases Recoverable Heat from Boiler Flue Gases can be cooled subject to criteria such as dew point, cold-end Recoverable Heat, MMBtu/hr corrosion, and economic heat Initial Stack Gas transfer surface. (See Exhaust Temperature, °F Boiler Thermal Output, MMBtu/hr Gas Temperature Limits.) 25 50 100 200 ■■ Study the cost-effectiveness of installing a feedwater economizer 400 1.3 2.6 5.3 10.6 or air preheater in your boiler. 500 2.3 4.6 9.2 18.4 600 3.3 6.5 13.0 26.1 Based on natural gas fuel, 15% excess air, and a final stack temperature of 250˚F. Example An 80% efficient boiler generates 45,000 pounds per hour (lb/hr) of 150-pounds-per-square-inch-gauge (psig) steam by burning natural gas. -
Performance Analysis of Air Preheater in 210Mw Thermal Power Station
Manivel .J, Manimaran .L, Thiyagarajan .M, Satheeshkumar .P; International Journal of Advance Research, Ideas and Innovations in Technology. ISSN: 2454-132X Impact factor: 4.295 (Volume3, Issue2) Performance Analysis of Air Preheater in 210mw Thermal Power Station J. Manivel1 L. Manimaran2 M. Thiyagarajan3 Department of Mechanical Engineering, Department of Mechanical Engineering, Department of Mechanical Engineering, SNS College of Engineering, SNS College of Engineering, SNS College of Engineering, Coimbatore, TN, India Coimbatore, TN, India Coimbatore, TN, India P. Satheeshkumar4 Thiruppathi .R5 Department of Mechanical Engineering, SNS College of Department of Mechanical Engineering, SNS College of Engineering, Coimbatore, TN, India Engineering, Coimbatore, TN, India s Abstract: The efficiency of boiler in thermal power station is greatly depending on the utilization of waste heat in the flue gas by air pre heater and economizer. The increasing in efficiency of boiler can be achieved by increasing the performance of air pre heater and economizer. Enhancing heat transfer rate by changing profile of air pre heater will lead to increasing in performance of the air pre heater and economizer. The changing profile and increasing heat transfer area will increase the heat transfer rate. In 210MW Mettur thermal power station, notched flat profile is used as heat transfer area in air pre heater segment. In order to improve heat transfer rate, notched flat profile are replaced by double undulated profile and single seal are replaced by double seal. Hence heat loss in the air pre heater is minimized. The performance of economizer is enhanced by increasing the diameter of the coils. Hence the economizer and air pre heater absorbs additional heat from exhaust flue gas. -
Designing and Maintaining Steam Coil Air Preheaters for Reliability And
PLANT AUXILIARY SYSTEMS Designing and maintaining steam coil air preheaters for reliability and effectiveness If engineered well and drained properly, a simple finned-tube heat exchanger can help maximize a fossil-fueled power plant’s combustion efficiency, capacity, and air pollution reduction. Use the guidelines in this article ei- ther to return a disabled steam coil air preheater to service or to improve the performance of a unit that may have been wasting steam and money for years. By James R. Smith, Armstrong Heat Transfer Group team coil air preheaters (SCAPs) are sitions and the duct connection to the inlet there (Figure 4). Clogging and reduced per- found in most fossil-fueled utility and (cold end) of an RRAH. As opposed to being formance will be the undesirable outcome. Slarge industrial power plants in North bolted in place by duct flanges (Figure 2), Often (but unintentionally), the SCAP’s coils America. Their primary function is to heat units used in such a configuration are usu- serve as a convenient platform for mainte- combustion air before it enters a rotary re- ally drawer-mounted, for easier access and nance workers tasked with cleaning and in- generative air heater (POWER, April 2006, p. removal (Figure 3). specting the RRAH. 72) or a traditional tubular air heater. Wheth- Placing a SCAP ahead of the cold end Another undesirable consequence of er a rotary regenerative air heater (RRAH) (inlet side) of a RRAH, however, can invite placing a poorly constructed, specified, or or a traditional tubular heater is downstream, maintenance problems and shorten unit life. -
Evaluation of Dry Fly-Ash Particles Causing Difficult Deposits for Acoustic Soot Blowing of Boilers
UPTEC Q16 025 Examensarbete 30 hp December 2016 Evaluation of dry fly-ash particles causing difficult deposits for acoustic soot blowing of boilers Arvid Bo Cedervall Abstract Evaluation of dry fly-ash particles causing difficult deposits for acoustic soot blowing of boilers Arvid Bo Cedervall Teknisk- naturvetenskaplig fakultet UTH-enheten This thesis compares ash collected from different boilers cleaned using infrasound cleaning. The samples were evaluated from their physical properties, in an attempt to Besöksadress: find connections between the difficulty to remove ash and its physical appearance. To Ångströmlaboratoriet Lägerhyddsvägen 1 get a deeper understanding of the mechanisms behind adhesion and fouling, and Hus 4, Plan 0 possibly explain results from the study of the ash samples, a literature review was carried out. The ash was also evaluated to see if any connections could be drawn Postadress: between the physical properties of the ash and its fouling capabilities. A strong Box 536 751 21 Uppsala connection was found between ash density and its fouling capabilities. It was found that no dry ash with a density higher than 0.4 g/ml were difficult to remove with Telefon: infrasound cleaning, and no ash with lower density was easy to remove. The ash 018 – 471 30 03 density was calculated from a measurement of the weight of a certain volume of ash Telefax: on a scale. Optical microscopy was used to study the ash samples, and gave an 018 – 471 30 00 estimation of particle size, shape, and porosity. However, no clear connection could be observed with this method between the different samples and which were difficult Hemsida: to remove. -
Improvement in Efficiency of Air Preheater in Boiler Tps- 1 Expansion
IJRDO - Journal of Mechanical and Civil Engineering ISSN-2456-1479 IMPROVEMENT IN EFFICIENCY OF AIR PREHEATER IN BOILER TPS- 1 EXPANSION S.Sudhakar* C.M.Raguraman Department of Mechanical Engineering, Faculty of Engineering and Technology, Annamalai University, Annamalai Nagar - 608002, India. e-mail: [email protected]. Abstract-- An air pre-heater is a general term to describe any The organization of this paper is as follows: device designed to heat air before another process (for Section I gives an Introduction and an outlay of the scope example, combustion in a boiler) with the primary objective of of the work. Proposed methodology is elaborated in increasing the thermal efficiency of the process. They may be Section II. Air and flue gas path is given in Section III, used alone or to replace a recuperative heat system or to and are described in Section V followed by the replace a steam coil. In particular, this project describes the combustion air pre-heaters used in large boilers found in conclusion in Section VI. thermal power stations producing electric power from e.g. fossil fuels, biomasses or waste. The purpose of the air pre- SCOPE THE WORK heater is to recover the heat from the boiler flue gas which increases the thermal efficiency of the boiler by reducing the After studying the journal papers mentioned above, it is useful heat loss of the flue gas in an regenerative pre-heater. understood that there are some leakages development in This project analysis how operation parameters of an the RAPH and maintenances of RAPH is to be considered regenerative air preheater can be optimized in order to for the improvement efficiency of the boiler shell and increase its efficiency and consequently the overall efficiency tube air preheater. -
Incinerators
EPA/452/B-02-001 Section 3 VOC Controls EPA/452/B-02-001 Section 3.2 VOC Destruction Controls EPA/452/B-02-001 Chapter 2 Incinerators William M. Vatavuk Innovative Strategies and Economics Group, OAQPS U.S. Environmental Protection Agency Research Triangle Park, NC 27711 Donald R. van der Vaart & James J. Spivey Research Triangle Institute Research Triangle Park, NC 27709 September 2000 Contents 2.1 Introduction ........................................................................................................................................... 2.-3 2.2 Process Description .............................................................................................................................................. 2-3 2.2.1 Thermal Incinerators .................................................................................................................. 2-6 2.2.2 Catalytic Incinerators ............................................................................................................... 2-10 2.2.3 Other Considerations: Packaged versus Field-Erected Units, Auxiliary Equipment ............... 2-13 2.2.4 Technology Comparison .......................................................................................................... 2-15 2.3 General Treatment of Material and Energy Balances ............................................................................ 2-16 2.4 Design Procedures ............................................................................................................................... 2-18 -
Improving the Overall Heat Transfer Coefficient of an Air Preheater by Design, Fabrication and CFD Analysis
International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 NATIONAL CONFERENCE on Developments, Advances & Trends in Engineering Sciences (NCDATES- 09th & 10th January 2015) RESEARCH ARTICLE OPEN ACCESS Improving the Overall heat transfer coefficient of an Air Preheater by Design, Fabrication and CFD Analysis M.Nageswara rao* *Assistant professor, Department of Mechanical Engineering, TKR Engineering College, Hyderabad. ABSTRACT An air preheater is a heat exchanger device designed to heat air before another process (for example, combustion in a boiler) with the primary objective of increasing the thermal efficiency of the process. The purpose of the air preheater is to recover the heat from the boiler flue gas which increases the thermal efficiency of the boiler by reducing the useful heat lost in the flue gas. This project mainly deals with design, modeling and fabrication and cfd analysis of a shell and tube air preheater. Over all heat transfer coefficient of the shell and tube heat exchanger is based on the results of effectiveness-ntu approach and lmtd approach. Drawing of various components will be presented with the help of various software’s like solid works, proe, etc., even different experimental results and trails will be analyzed and tabulated. Conclusion of the project will be the complete presentation of thermal and mechanical design, fabrication model, Overall heat transfer coefficient and cfd (computational fluid dynamics) analysis for the air preheater. Keywords: air preheater, cfd, fabrication . I. INTRODUCTION modeling and fabrication of shell and tube air An air pre-heater is a general term to describe preheater including thermal design. any device designed to heat air before another process (for example, combustion in a boiler) with III. -
Steam Boilers & Industrial Furnaces
Sustainable Power Generation MJ2405 Steam Boilers & Industrial Furnaces Miro Petrov Dept. of Energy Technology, KTH - Stockholm 1 Reading material on boilers Many books can be used – Any chapter on combustors, boilers, furnaces, steam generators, etc., might be good to look through! The main suggested sources: Advanced Energy Systems (Khartchenko&Kharchenko), CRC Press 2014 – section 3.7 and parts of chapters 6 & 7. Energy Conversion – free e-book by courtesy of the University of Tulsa, Kenneth C. Weston, 2000 – parts of chapters 4 and 9 http://www.personal.utulsa.edu/~kenneth-weston/ På svenska: Energiteknik - Del 2; Henrik Alvarez, Studentlitteratur 2006 – delar av kapitel 9 & kapitel 10. Dept. of Energy Technology, KTH - Stockholm 2 Horizontal fire-tube water heater Source: www.steamshowersauna.org Simplest boiler type. Used typically to produce hot water or saturated steam. The combustion zone (the flame) is inside a tube immersed in a water tank. Fired with liquid or gas fuels. Mostly at small- to mid-scale district heating or industrial applications. Not suitable for large sizes or for solid fuels. Dept. of Energy Technology, KTH - Stockholm 3 Purpose and parts of a large steam boiler • Should properly be called a “steam generator”! • Burns fuel to produce hot gases in the combustion zone (furnace) which then transfer heat to the water/steam side in the steam generation zone. Alternatively, some available waste hot gases from another process can be used, instead of burning a fuel. • The steam generation zone consists of economizer (water heater), evaporator (boiling section), and superheater/reheater situated along the flue gas path. • Remaining heat from the flue gas is transferred back to the fresh air supplied to the combustion zone, via an air preheater. -
Sweden 728 Sweden Sweden
SWEDEN 728 SWEDEN SWEDEN 1. GENERAL INFORMATION 1.1. General Overview Sweden is a long narrow country in the northern part of Europe and borders Norway in the west, Finland in the north east and the Baltic Sea in the South and east, as shown in Figure 1. The total length from north to south is 1,600 kilometres and the land area is 410,932 square kilometres. The size of the area is the third in Western Europe after France and Spain. The area is almost twice as big as that of Great Britain. The north-west part of Sweden consist of mountains with a slope towards the east. There are many rivers in the north and lakes are scattered all over the country. Sweden’s coast line is more than 2,000 kilometres long. FIG. 1. Location of Sweden in Europe. The northern boundary is about 250 kilometres north of the north polar circle 66°30´, but because of the Gulf Stream coming from west, the climate is not of a polar type. The average temperature over the year varies between -1.5 °C in the north to 7.8 °C in the south. The population data in Table 1 show a very slow increase of the population. In 1998, Sweden had 8.9 million inhabitants. The population density is 21.6 persons per square kilometres, however, the northern part of Sweden is sparsely populated with smaller than 20% of the inhabitants living in the northern half of the country. SWEDEN 729 There are no other domestic energy sources except hydro and bioenergy (used mainly in the pulp and paper industry) exploited. -
College of Engineering and Technology, Akola
College of Engineering & Technology Akola COLLEGE OF ENGINEERING AND TECHNOLOGY, AKOLA DEPARTMENT OF MECHANICAL ENGINEERING NAME : ................................................................... SUBJECT : ENERGY CONVERSION LAB CLASS : SECOND YEAR MECHANICAL ENGG. ROLL NO : .............. NAME OF THE FACULTY: ROSHAN D. BHAGAT DESIGNATION: ASSIST. PROFESSOR BRANCH: MECHANICAL ENGINEERING SUBJECT: EC-1LAB SEMESTER: FOURTH ACADEMIC YEAR 2016-2017 1 ENERGY CONVERSION-1 LAB College of Engineering & Technology Akola DEPARTMENT OF MECHANICAL ENGINEERING CERTIFICATE This is to certify that Mr. / Miss............................................. has satisfactorily completed the course of experiments in ENERGY CONVERSION LAB as prescribed by the Sant Gadge Baba Amravati University in the laboratory of college for the academic year 2016-2017 Date: Signature of Teacher In charge of the Batch Head of department Name of the candidate Registration no Roll no. Date of practical examination 2 ENERGY CONVERSION-1 LAB College of Engineering & Technology Akola INDEX SR.NO NAME OF EXPERIMENT DATE SIGN 1 Study of water tube boiler babcock and Wilcox 2 Study of locomotive boiler 3 Study of high pressure boiler 4 Study of boiler accessories 5 Trial on boiler and heat balance sheet 6 Study of boiler mounting 7 Study and trial on steam turbine 8 Study of condenser 9 Study of condensate and air extraction pump 10 Study of steam power plant 3 ENERGY CONVERSION-1 LAB College of Engineering & Technology Akola Practical No 1 Aim: Study of water tube Babcock and Wilcox water tube boiler Apparatus: Babcock and Wilcox water tube boiler Theory: The water tube boiler used exclusively when pressure above 10 bars and capacity in excess of 7000 kg of steam per hour is required. -
Improved Performance of a Industrial Packaged Boiler by Use
ISSN(Online) : 2319-8753 ISSN (Print) : 2347-6710 International Journal of Innovative Research in Science, Engineering and Technology (An ISO 3297: 2007 Certified Organization) Website: www.ijirset.com Vol. 6, Issue 1, January 2017 Improved Performance of a Industrial Packaged Boiler by Use of Economizer Nishadevi Jadeja1, Sanjaysinh Zala2 Assistant Professor, Dept of Mechanical Engineering, Govt. Engg. College, Bhavnagar, Gujrat , India1 Assistant Professor, Dept of Mechanical Engineering, Govt. Engg. College, Bhavnagar, Gujrat , India2 ABSTRACT: In the present scenario energy losses in the industrial boilers are majour problems so carryout energy audit at Anish chemicals Gidc chitra, at Bhavnagar. By energy Audit calculated boiler efficiency and major losses in plant and this work is completed . We can improved boiler efficiency by utilize economizer and give maximum cost benifit analysis. The value of boiler efficiency and diffrent losses are calculated at Anish chemicals .It is a combined water and fire tube boiler using biomass coal as fuel. Boiler efficiency calculated by direct method is in range of (78.5% to 81.6%). Major losses from boiler are heat loss due to radiation and convection from non insulated surfaces (4.8% to 6.3%), heat loss due to flue gas (6.3% to 6.4%), heat loss due to blow down (0.263 to 0.398%), heat loss due to incomplete combustion (1.87% to 2.21%), heat loss due to unburnt coal in bottom ash (1.74 % to 1.86)and heat loss due to moisture present in fuel (1.3% to 1.6%).Shell and tube type heat exchanger (economizer) was designed to recover heat loss due to flue gas by reducing flue gas discharge temperature. -
CARL RICHARD SODERBERG February 3, 1895–October 17, 1979
NATIONAL ACADEMY OF SCIENCES C A R L R IC H A R D S ODER B ER G 1895—1979 A Biographical Memoir by ASC H E R H . ShAP IRO Any opinions expressed in this memoir are those of the author(s) and do not necessarily reflect the views of the National Academy of Sciences. Biographical Memoir COPYRIGHT 1998 NATIONAL ACADEMIES PRESS WASHINGTON D.C. Courtesy of MIT Museum, Cambridge, Massachusetts CARL RICHARD SODERBERG February 3, 1895–October 17, 1979 BY ASCHER H. SHAPIRO HE RICH INSPIRING life of C. Richard (“Dick”) Soderberg, TInstitute Professor emeritus at the Massachusetts Insti- tute of Technology came to an end at age eighty-four. With roots in the simple realities of a boyhood in a fishing family on a remote Swedish island in the Baltic Sea, his qualities of mind and character led him first into a distinguished industrial career as an engineer in his adopted country, the United States. He went on to an illustrious career in engi- neering education, with remarkable consulting activities on the side. His years were marked by an expansive and seem- ingly unlimited passion to learn, by a capacity to teach, by a superb intuitive sense of design and rightness, by an unflag- ging breadth of intellectual interest, by a deep understand- ing of the social and historical forces set in motion by tech- nology, and by a warmth and nobility of spirit that endeared him to his colleagues and friends. Three major phases in his professional life were espe- cially notable. First, at the Westinghouse Electric & Manu- facturing Company he was instrumental in solving the prob- lems of steam turbines as these progressed to ever larger sizes and higher operating pressures and temperatures.